Catalyst and process for producing methacrylic acid

ABSTRACT

A catalyst composition useful for the oxidation of unsaturated aldehydes, particularly the oxidation of methacrolein to produce methacrylic acid, comprises the combination of oxides of molybdenum, copper, phosphorus, antimony, and cesium in predetermined relative atomic ratios.

PRIOR ART

This invention relates to a process and catalyst for the vapor-phaseoxidation with molecular oxygen of methacrolein to methacrylic acid.

It is well known that unsaturated acids, such as acrylic acid andmethacrylic acid, can be produced by the vapor-phase oxidation of thecorresponding unsaturated aldehydes by means of molecular oxygen in thepresence of a suitable oxidation catalyst. A variety of catalystcompositions have been proposed for this purpose. Many such compositionscomprise the oxides of molybdenum and phosphorus in association with theoxides of various other elements, both metallic and non-metallic.

For example, and with respect to the catalyst to be discussed hereafter,British Pat. No. 1,430,337 and U.S. Pat. No. 4,000,088 propose the useof a catalyst composition in which the oxides of molybdenum andphosphorus are combined with the oxides of antimony, copper andoptionally, chromium. The catalyst does not contain cesium.

U.S. patents in which cesium may be present in similar catalysts include4,051,179 and 4,042,533. In '179 copper and vanadium are treated asalternatives, while an alkali metal must be included, but antimony isconsidered optional. In '533 tungsten is required, while copper andphosphorus are optional and antimony is lacking.

Despite the disclosures of the prior art, a catalyst of this type is notformulated merely by combining the many elements which have beendisclosed in the prior art. Instead the catalyst performance must bedetermined experimentally at the expected operating conditions. Smallchanges in composition may be very important in achieving improvedcatalyst performance and particularly in optimizing the catalystcomposition to suit a specific reaction and set of operating conditions.The point is well illustrated by the improvements in catalystformulation to be described hereinafter.

It has been found that catalysts for oxidation of methacrolein tomethacrylic acid have the characteristic property of remaining stablefor a long period of time and then, without warning, of beginning arapid decline in activity. Consequently, an increase in the useful lifeof such catalysts has been sought, which has been achieved in thepresent invention by the addition of a stabilizing ingredient.

SUMMARY OF THE INVENTION

It has been discovered that when using the catalysts to be described toproduce methacrylic acid by vapor phase oxidation of methacrolein, it ispossible to achieve both high activity and high selectivity for asignificantly improved useful life compared to catalysts which lack thestabilizing element of the invention. The catalyst composition comprisesoxides of molybdenum, copper, phosphorus, antimony, and cesium inpredetermined relative atomic ratios. More specifically, the catalystcomposition of the invention comprises the oxides of the above specifiedelements in the following atomic ratios: Mo=12, Cu=0.05-3, P=0.1-5,Sb=0.01-3, and Cs=0.1-3. The catalyst composition may be regarded eitheras a mixture of oxides of the named elements or as oxygen-containingcompounds of the elements or both.

The catalyst composition used in the process of the invention also maybe expressed by the following general formula:

    Mo.sub.a Cu.sub.b P.sub.c Sb.sub.d Cs.sub.e O.sub.f

wherein a to f indicate the atomic ratio of each component and, when ais 12, b is 0.05-3, c is 0.1-5, d is 0.01-3, e is 0.1-3, and f has avalue which is determined by the valence and proportions of the otherelements in the catalyst.

When such a catalyst as has been described is in contact with avapor-phase mixture of methacrolein, molecular oxygen, steam, andnitrogen at temperatures in the range of 250°-400° C. and pressures inthe range of 0-5 atmospheres, excellent activity and selectivity to theproduction of methacrylic acid is obtained for a longer period of timethan for a catalyst lacking cesium.

BRIEF DESCRIPTION OF THE DRAWING

The sole FIGURE graphically displays the change of reaction temperatureover a period of operation as a comparison of the useful life ofoxidation catalysts.

DESCRIPTION OF THE PREFERRED EMBODIMENTS Catalyst Composition andPreparation

The catalyst of the invention comprises oxides or oxygen-containingcompounds of molybdenum, copper, phosphorus, antimony and cesium inpredetermined atomic ratios, as expressed in the following generalformula: Mo_(a) Cu_(b) P_(c) Sb_(d) Cs_(e) O_(f) wherein a to f indicatethe atomic ratio of each component and, when a is 12, b is 0.05-3, c is0.1-5, d is 0.01-3, e is 0.1-6, and f is a value determined by thevalence and proportions of the other elements in the catalyst. Otherelements, which may be included in minor amounts in the catalystformulation in order to promote catalyst activity or selectivity andwithout losing the advantages to be shown for the principal formula, areconsidered to be within the scope of the invention. The catalystcomposition may be regarded either as a mixture of oxides of the namedelements or as oxygen-containing compounds of the elements or both. Asprepared and/or under reaction conditions, the catalyst may containeither or both forms and both are intended to be included within thephrase "mixtures of oxides."

The catalyst composition is preferably used in unsupported form, e.g. inthe form of pellets or other like compressed shapes of various sizesalthough conventional supports could be employed instead. Thecomposition may be formed in conventional manner using techniques wellknown to persons skilled in the art. For example, compounds ofmolybdenum, copper, phosphorus, antimony and cesium are dissolved in asmall amount of water or other solvent, and the solutions are thencombined and evaporated to dryness, e.g. in a rotary dryer. The severalcomponents can be introduced into solution in the form of various saltsor other compounds of convenient types and no specific form for thecatalyst precursors is necessary. The use of ammonium salts, halidese.g. chlorides, nitrates or acid forms of the elements, e.g. phosphoricacid, are, however, particularly suitable. Preferably, however, aqueoussolutions are employed and water-soluble forms of the elements are used.In some cases the solutions may have acids and/or bases added to them tofacilitate dissolution of the catalyst precursors. For example, acidssuch as hydrochloric or nitric acid, or bases such as ammoniumhydroxide, can be used as desired. The resulting powder from theevaporation is then thoroughly dried and preferably screened toeliminate large particles which make it difficult to produce uniformcompressed shapes, such as pellets. Typically, the powder is passedthrough a 20-mesh screen. The powder is then mixed with an organicbinder which can be of any conventional type, such as polyvinyl alcohol,and the mixture is thoroughly dried and again screened, typically toprovide a 20-80 mesh size. The dried mixture is then preferably combinedwith a lubricant, again of any conventional type, such as stearic acidor graphite, and compressed into the desired shape, e.g. pelletized, thecompressed shapes typically having heights and diameters of 1/16 inch to3/8 inch. Finally, the thus produced catalyst composition is activatedat high temperature for a prolonged period in accordance withconventional practice in this art. For example, the pellets are placedin an oven or kiln, or in a tube through which air is passed, at anelevated temperature (e.g. 300°-500° C., preferably 325°-450° C.) for atleast ten hours. In a particularly preferred activation step, thetemperature is raised at the rate of 20° C. per hour to a maximum of420° C., preferably 320°-400° C., and this temperature is maintained for16 hours.

It will be understood that the foregoing description regardingpreparation of the catalyst in a form suitable for use in a vapor-phaseoxidation reaction is merely illustrative of many possible preparativemethods, although it is a particularly suitable method and is preferred.

Methods of Operation

The catalysts described are generally useful for the production ofunsaturated acids by oxidation with molecular oxygen of unsaturatedaldehydes, although the reaction of methacrolein to form methacrylicacid is of particular interest. Other possible starting materials arethe monoethylenically unsaturated aliphatic monoaldehydes of from 3 to 6carbon atoms, such as acrolein, crotonaldehyde, 2-methyl-2-butenal, andthe like, or mixtures thereof.

The reaction in which the catalyst compositions of this invention are ofparticular utility and in which they provide high conversions andselectivities involves contacting the catalyst with methacrolein andoxygen in the vapor phase, preferably also in the presence of steam anddiluents. When the catalyst of this invention is used in the vapor-phaseoxidation of methacrolein to form methacrylic acid, the oxidationconditions employed are those generally associated with this reaction,although the molar ratio of oxygen to methacrolein should be kept at ahigh value near the flammable range in order to obtain the longestuseful catalyst life. Once reaction is begun, it is self-sustainingbecause of its exothermic nature. A variety of reactor types may beemployed, such as fluid or fixed bed types, but reactors having thecatalyst disposed inside a multiplicity of heat exchanger tubes areparticularly useful and convenient.

The gaseous feed to the reactor contains appropriate concentrations ofmethacrolein, oxygen and steam and usually an inert gas, such asnitrogen, is also present. The oxygen is usually added as such or asair, which may be enriched with oxygen. As mentioned, conventionaloxidation conditions can be employed but it is a feature of the catalystof this invention that the methacrolein can be present in concentrationsof more than 5 up to about 20 volume percent of the total feed with apreferred range of more than 5 up to about 15 volume percent. In generalat least 6 volume percent of the aldehyde is used in the feed. Thecorresponding ranges for oxygen are 3 to 15 volume percent, preferably 5to 12 volume percent and for steam up to 50 volume percent, preferably 5to 35 volume percent, the balance being the inert gas or gases.

The temperature of the reaction should, for best results, be within therange of from about 270° to 450° C., preferably 280°-400° C., and theoptimum temperature range is 290° to 325° C. Because the reaction isexothermic, means for conducting the heat away from the reactor arenormally employed to avoid a temperature increase which favors thedestruction of methacrolein by complete oxidation to carbon dioxide andwater. The reactor temperature may be controlled by conventional methodssuch as by surrounding the catalyst-containing tubes with a molten saltbath.

The reaction may be conducted at atmospheric, superatmospheric orsubatmospheric pressure. Preferably, however, pressures ranging fromatmospheric up to about 8 kg/cm² absolute, preferably up to about 6.3kg/cm² absolute, and most preferably up to about 4.5 kg/cm² absolute areemployed.

The unsaturated acid product may be recovered by a number of methodswell known to those skilled in the art. For example, the acid may becondensed, or scrubbed with water or other suitable solvents, followedby separation of the unsaturated acid product from the scrubbing liquid.The gases remaining after the acid-removal step are suitably recycled tothe reaction, if desired, preferably after removal of CO₂ byconventional means, e.g., absorption in aqueous carbonate solution.

The features of the invention will be more readily apparent from thefollowing specific examples of typical catalyst preparation and its usein the oxidation of methacrolein. It will be understood, however, thatthese examples are for the purpose of illustration only and are not tobe interpreted as limiting the invention.

EXAMPLE 1

In 750 cc of water are dissolved 636 grams of (NH₄)₆ Mo₇ O₂₄.4H₂ O. Then21.7 grams of Cu(NO₃)₂.3H₂ O are dissolved in 100 cc of water, 58.4grams of CsNo₃ are dissolved in 300 cc of water, 20.5 grams of SbCl₃ aredissolved in a mixture of 30 cc of water, and 10 cc of concentrated HCland 34.5 grams of H₃ PO₄ are dissolved in a mixture of 100 cc of water.These solutions are fed to a rotary dryer of 4,000 cc capacity and themixture is evaporated to dryness at a temperature of 140° C. Theresulting powder is removed from the dryer and dried in an oven at 200°C. for 12 hours. The dried powder is screened through a 20-mesh screen,a 4% aqueous solution of polyvinyl alcohol is added in sufficientquantity to make a damp mixture and this mixture is dried at 75°-80° C.until the moisture content falls to 2-4 wt. %. The dried mixture is thenscreened to 20-80 mesh size particles, and about 2-6% of stearic acidpowder is thoroughly mixed with it. The resulting mixture is thenpelletized to form pellets of 3/16 inch height and diameter in which thecatalyst components molybdenum, copper, phosphorus, antimony, and cesiumare present in the atomic ratios of 12, 0.3, 1, 0.3 and 1, respectively.The pellets are then activated in an oven by heating them gradually at arate of 20° C. per hour to 380° C. and maintaining them at thistemperature for 16 hours. The activated pellets have a density of 0.97gm/cc.

EXAMPLE 2

A 150 cc quantity of the catalyst composition is placed in a reactordefined by a 1/2"×90" stainless steel pipe, the reactor pipe beingfilled with 50 cc of inert filler (silicon carbide) below the catalystbed and 100 cc of the inert filled above the catalyst bed inconventional manner to insure uniform temperature contact with thecatalyst. Nitrogen-diluted mixtures containing methacrolein, oxygen andsteam are fed to the reactor at a pressure of 1.74 kg/cm² (absolute) andat a space velocity of about 1200 hr⁻¹. The term "space velocity" isused in its conventional sense to mean liters of gas (at standardtemperature and pressure) per liter of catalyst per hour. The feedcomposition is approximately, by volume, 6-7% methacrolein, 11-12%oxygen and 20% steam, the balance being nitrogen, determination beingmade on a wet basis. The reaction is run continuously and the exit gasis analyzed at intervals of several hours to give the overall effect ofa series of different runs. Analyses are carried out by means of gaschromatography and by infrared spectrography using conventionaltechniques.

For comparison of many catalysts, all of which are capable of providinga satisfactory yield of methacrylic acid, but which differ in theiruseful life, an accelerated aging test is carried out on the catalyst ofExample 1 and reported in the sole FIGURE. The catalyst is tested undersevere conditions in order to obtain relatively quick determination ofthe catalyst performance by raising the operating temperature to thelevel needed to achieve at least about 80% conversion of methacrolein tomethacrylic acid. For commercial operation, the temperature mostsuitable for obtaining the best yield of methacrylic acid for a longperiod of useful catalyst life would be selected. As the catalystdeactivates, it is necessary to raise the operating temperature tomaintain a constant degree of methacrolein conversion. The upper limitof catalyst temperature is reached when the target of 80% conversion canno longer be obtained. This is generally found to be at about 325°-330°C. At that point, the catalyst is no longer useful. While for commercialoperation a useful life of at least 2-3000 hours is desired, by means ofthe accelerated aging test, even durable catalysts can be fullydeactivated within about 100 hours, thus providing catalyst lifeinformation which might be obtained only after thousands of hours undermore conventional conditions.

The performance of a catalyst containing cesium is shown in the FIGURE.The useful life in the accelerated test of a catalyst containing cesium(Example 3) is about 70 hours and it begins to lose activity after aninduction period of about 30 hours. The performance of a catalystcontaining no cesium is markedly inferior as will be seen in thefollowing comparative example.

COMPARATIVE EXAMPLE EXAMPLE 3

A catalyst corresponding to that of Example 1 is prepared by the sametechnique except no cesium nitrate is included in the initial solutionto provide a catalyst similar to that of U.S. Pat. No. 4,000,088 andhaving the following nominal composition:

    Mo.sub.12 Cu.sub.0.3 P.sub.1 Sb.sub.0.3 O.sub.i

When the catalyst is tested under the conditions of Example 2 it isfound that the results cannot be plotted in the FIGURE for comparisonwith Example 2. Even at 370° C., only 50% conversion of methacrolein wasobtained, with 70% selectivity to methacrylic acid. Since the FIGUREshows the temperature required to obtain 80% conversion, it is notpossible to plot the results.

The advantage of adding cesium is apparent when comparing the results ofExamples 2 and 3. With no cesium present, the catalyst is not capable ofreaching a high conversion level, which is important for commercialapplication. Example 3 indicates that addition of the alkali metalcesium improves the catalyst of Example 1.

What is claimed is:
 1. A cataylst composition suitable for thevapor-phase oxidation of methacrolein to produce methacrylic acid havingthe formula Mo_(a) Cu_(b) P_(c) Sb_(d) Cs_(e) O_(f) where: a=12;b=0.05-3; c=0.1-5; d=0.01-3; e=0.1-3; and f=value determined by thevalence and proportions of the other elements of the formula.